First Law of Thermodynamics State Functions - A State Function is a thermodynamic quantity whose value depends only on the state at the moment, i. e., the temperature, pressure, volume, etc… - The value of a state function is independent of the history of the system. - Temperature is an example of a state function. - The fact that temperature is a state function is extremely useful because it we can measure the temperature change in the system by knowing the initial temperature and the final temperature. - In other words, we don’t need all of the nitty-gritty detail of a process to measure the change in the value of a state function. - In contrast, we do need all of the nitty-gritty details to measure the heat or the work of a system. Reversibility A reversible process is a process where the effects of following a thermodynamic path can be undone be exactly reversing the path. An easier definition is a process that is always at equilibrium even when undergoing a change. Phase changes and chemical equilibria are examples of reversible processes. Ideally the composition throughout the system must be homogeneous. - This requirement implies that the no gradients, currents or eddys can exist. - To eliminate all inhomogeneities, a reversible process must occur infinitely slow! 1
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First Law of Thermodynamics
State Functions- A State Function is a thermodynamic quantity whose value depends only on the
state at the moment, i. e., the temperature, pressure, volume, etc…
- The value of a state function is independent of the history of the system.
- Temperature is an example of a state function.
- The fact that temperature is a state function is extremely useful because it we can measure the temperature change in the system by knowing the initial temperature and the final temperature.
- In other words, we don’t need all of the nitty-gritty detail of a process to measure the change in the value of a state function.
- In contrast, we do need all of the nitty-gritty details to measure the heat or the work of a system.
Reversibility
A reversible process is a process where the effects of following a thermodynamic path can be undone be exactly reversing the path.
An easier definition is a process that is always at equilibrium even when undergoing a change.
Phase changes and chemical equilibria are examples of reversible processes.
Ideally the composition throughout the system must be homogeneous.- This requirement implies that the no gradients, currents or eddys can exist.- To eliminate all inhomogeneities, a reversible process must occur infinitely
slow! - Thus no truly reversible processes exist. However, many systems are
approximately reversible. And assuming reversible processes will greatly aid our calculations of various thermodynamic state functions.
Reversibility during pressure changes ensures that
p = pex
That is, the pressure on the inside of the container is always equal to the pressure exerted on the outside of the container.
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Theorem of Maximum Work
The maximum amount of work that can be extracted from an expansion process occurs under reversible conditions.
Thus the theorem implies that during an irreversible expansion, some of the energy is lost as heat rather than work. The inhomogeneities (currents, gradients and eddys) in pressure that occur during an irreversible process are responsible for the heat.
Initial Definitions of Energy and Energy Transfer
Internal Energy- Sum of the kinetic and potential energy in a sample of matter.
Microscopic modes of Internal Energy (20th century view)- degrees of freedom for energy storage
translationalrotationallibrational – vibrations caused by intermolecular forcesvibrationalelectronicnuclear, etc…
- more specifics in second semester- unnecessary for understanding of thermodynamics but sometimes helpful.
Macroscopic view of internal energy (19th century view)- A reservoir of energy within the sample.- The details of the energy are unknown.
Internal energy is a state function.
WorkRecall the definition of work from classical mechanics.
Microscopically, work involves the concerted motion of molecules (that is, molecules moving in one direction.)Work is a transfer of energy, not a quantity of energy.Work is not a state function.
-calculation of work depends on thermodynamic path (as seen from definition)
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A more thermodynamically useful rearrangement (let F = pA and dV = dlA) is
- the negative sign is a sign convention (discussed below)- pex is the external pressure (the pressure outside the container)- pex is used in definition because we really do not know what kind of pressures
develop during a thermodynamic change. - i.e., pressure currents and eddies are likely for an arbitrary change.
Other forms of work are possibleElectrical work
Polarization work (e.g., piezoelectricity)
Surface tension
Twisting work
Sign conventions for work-w – work done by system (expansion for pV work)+w – work done on the system (compression for pV work)
Heat- macroscopically heat is a thermal energy transfer
- energy transfer usually characterized by temperature and the zeroth law of thermodynamics.
- microscopically heat transfer comes from- inelastic collisions- energy transfer from one molecule to another in multiple (every) direction
Sign conventions for heat
-q – heat transferred away from body (heat lost)+q – heat transferred into body (heat gained)
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First Law of Thermodynamics
The physicists that studied energy changes recognized that the energy of an object could be changed via heat or work.
James Joule demonstrated experimentally the law of conservation of energy, that is, that energy is not gained or lost, but merely transferred from one object to another. The law of conservation of energy is also known as the first law of thermodynamics. Since energy changes can be expressed only as heat or work, the first law of thermodynamics has the mathematical expression
Subtle points to make:1) q and w are energy changes, writing q and w is improper.
- We can’t refer to object having an amount of heat or work. The object has internal energy, enthalpy, free energy, etc…
2) The form of the first law of thermodynamics depends on the sign convention chosen for heat and work. Older texts state that ; however, the sign convention for work is different,
Differential Form of the First Law
The differential form of the first law is written as
The differential forms of heat and work are written with the slash to emphasize that they are inexact differentials.
Constant volume heat
During a constant volume process, w = 0. Therefore
That is, constant volume heat is equal to a change in the free energy.
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Measureable thermodynamic quantities
Thermal expansivity
The thermal expansivity is the measure of how a material changes its volume as the temperature changes.
Isothermal compressibility
The isothermal compressibility is the measure of how a material changes its volume as the pressure changes. Almost always, volume will decrease with increasing pressure, therefore, a negative sign is included in the definition to allow for the tabulation a positive values.
Both definitions modify an extensive change, or , into an
intensive change by dividing the change by the volume.
Enthalpy
BackgroundIn order to fully explain his ideas of free energy, Josiah Willard Gibbs needed to construct an energy state function that had the definition
H = U + PV
Gibbs named the quantity the heat content because a change in the quantity corresponded to heat gained or lost by a system at constant pressure provided no non-pV work is being done, that is.
Kamerlingh Onnes eventually named the function, H the enthalpy and the name stuck.
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Heat capacity- Heat is proportional to mass.- Heat is proportional to temperature difference.- Proportionality constant for a specific substance is the heat capacity or specific
heat.
Definition of Constant Pressure Heat Capacity – Cp
Since constant pressure heat is a change in enthalpy, the constant pressure heat capacity can be rewritten as
This quantity is one of the easily measurable quantities that is very important in thermodynamics.
Definition of Constant Volume Heat Capacity – Cv
Since constant volume heat is a change in internal energy, the constant volume heat capacity can be rewritten as
This quantity is another one of the easily measurable quantities that we will use a great deal in thermodynamics studies.
Relationship between Cp and CV
One way of examining the difference between internal energy and enthalpy is by examining the difference between the constant pressure heat capacity and the constant volume heat capacity.
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At this point, we want to find another expression for since it is not an easily
measurable quantity. We can find an alternative expression for based the total
differential of the internal energy.
The internal energy is a function of temperature and volume, thus the total differential is
Dividing the total differential by dT under constant pressure conditions yields
Two of the partial derivatives in this expression should be familiar:
and . Remember the thermal expansivity is
Let us substitute our result into the original equation for Cp – CV ,
What is the relationship between Cp – CV for an ideal gas?
Remember that for an ideal gas , therefore
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The relationship can be rewritten in terms of molar heat capacities.
This relationship is very important and worth memorizing.
Why is Cp greater than CV?- Heat capacity is substance’s capacity to store energy.- A substance that can store energy via work has a greater heat capacity than a
substance that has its volume kept constant.
Heat Reexamined
Isothermal Heat
Isochoric Heat
If CV is independent of temperature, (fair assumption for small temperature changes), then
Isobaric Heat
Adiabatic Heat
By definition, q = 0
All of the above results are free from assumptions (unless noted).
Thermochemistry
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Extent of Reaction
To monitor the progress, a variable known as the extant of reaction is defined as
where ni is the number of moles of chemical species i, ni,0 is the initial number of moles of chemical species i and i is the stoichiometric coefficient of the chemical species i for the specific reaction occurring.
When the extent of reaction is defined this way, the value of the extant of reaction does not depend on the chemical species used to examine the state.
Example: Consider the reaction P4 (s) + 5 O2 (g) 2 P2O5 (s). Suppose we start with 3 moles of phosphorus and 15 moles of oxygen.
a) What is the extant of reaction when 4 moles of P2O5 has been created?
Note: How much P4 has been consumed to create 4 moles of P2O5? A: 2 moles.
b) What is the extant of reaction when 2 moles of phosphorus has reacted?
The definition includes the stoichiometric coefficient to put the changes of the all the chemical species on an equal footing.
Soon we will be dealing reaction energies and other quantities specific to reactions. The reaction energies need to be intensive quantities and yet each chemical species may have a different amount. Thus reaction energies are defined with respect to the extent of reaction so that the specific chemical species is not important, but the reaction as a whole is important.
Standard States
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Standard Pressure - p
Thermodynamic quantities are measured with respect to a pressure of 1 bar (100.000 kPa)
Standard Temperature - T
Thermodynamic quantities are measured with respect to a temperature of 25 C (298.15 K)
Standard Concentration- c
Thermodynamic quantities are measured with respect to a concentration of 1m (that is 1 molal).
- Molal is used as a concentration unit rather than molar because molal is independent of temperature.
Biological Standard State
The biological standard state is a pressure of 1 bar, a temperature of 37 C and pH of 7, (that is [H+] = 1.0 10-7).
Hess’ Law
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Since enthalpy is a state function, we can choose more than one thermodynamic path to calculate a state function.
For chemical changes, Hess’ Law states that the enthalpy of a reaction can be calculated from the enthalpies of all of the chemical step processes needed for the chemical reaction.
In other words, if reactions can be added together to form a resultant reaction, then enthalpies of the step reactions can be added to find a resultant enthalpy of reaction.
Example: Calculate the enthalpy of reaction for the following reaction: 2 Al(s) + 3 Cl2(g) 2 AlCl3(s), given the reactions below.
2 Al(s) + 6 HCl(aq) 2 AlCl3(aq) + 3 H2(g) H = -1049 kJ/molHCl(g) HCl(aq) H = -74.8 kJ/molH2(g) + Cl2(g) 2 HCl(g) H = -185 kJ/molAlCl3(s) AlCl3(aq) H = -323 kJ/mol
Rearrange the equations such that their sum is the reaction of interest.
2 Al(s) + 6 HCl(aq) 2 AlCl3(aq) + 3 H2(g) H = -1049 kJ/mol6[HCl(g) HCl(aq)] H = 6[-74.8 kJ/mol]3[H2(g) + Cl2(g) 2 HCl(g)] H = 3[-185 kJ/mol]2[AlCl3(aq) AlCl3(s)] H = 2[+323 kJ/mol]
Constant Pressure Calorimeter- coffee cup calorimeter- open to atmosphere- appropriate for solution chemistry
Constant Volume Calorimeter- bomb calorimeter- sealed and isolated- appropriate for gas phase chemistry
Adiabatic Calorimeter- heat measured by temperature needed to keep thermal energy constant.
Process of measuring heat of combustion with bomb calorimeter1. Mass wick used to start combustion.2. Mass water used to absorb heat.3. Mass standard (benzoic acid) to be combusted4. Add water to combustion chamber to ensure that water from combustion will be
in liquid phase.5. Load standard and seal6. Fill combustion chamber with oxygen ( 25 atm)7. Begin combustion and record temperature change of water.8. Calculate heat capacity of calorimeter from standard
- need to account for heat of wick, and heat capacity of water.9. Repeat process with sample.
- with heat from wick, heat from the water and heat from the calorimeter, the heat of combustion of sample can be calculated.
Hess’ law is often used to the enthalpy of formation of a substance after its enthalpy of combustion has been calculated.
Example: 0.523 g of the military explosive, cyclotetramethylenetetranitramine (HMX), C4H8N8O8 is combusted in a bomb (!) calorimeter and an internal energy change of – 4.620 kJ is measured. Calculate the enthalpy of formation for HMX.
First write a balanced equation for its complete combustion.
Temperature Dependence of Internal Energy and Enthalpy
Recall that and
These relationships imply that we can find the internal energy or enthalpy at a nonstandard temperature as long as we know the heat capacity.
and
Integrating both sides of these equations yields
and
For large temperature changes, we can’t assume that the heat capacity is independent of temperature. Thus to calculate the internal energy or enthalpy at a nonzero temperature, we need the temperature dependence of the heat capacity.
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Example: Calculate the change in enthalpy of H2 (g) from 373 K to 1000 K, given that the constant pressure heat capacity has the form where d = 27.28 J/K mol, e = 0.00326 J/K2 mol and f = 0.00050 J K/mol.
Kirchoff’s law
That is by taking a stoichiometric sum of the heat capacities and integrating over the temperature range, we can find the correction to the reaction enthalpy at a non standard state temperature.
Example: 471 kJ/mol is the reaction enthalpy under standard conditions for the following reaction: 2 Fe2O3(s) + 3 C(s) 4 Fe(s) + 3 CO2(g). What is the reaction enthalpy at 1000 K?
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According to the NIST Webbook Internet site, the constant pressure heat capacities of the chemical species in the above smelting process can be fitted according to the Shumate equation,
The values for A, B, C, D and E for each species are given below.
Kirchoff’s Law can be stated with in a differential form as well.
Include and
Bond Enthalpies
A bond enthalpy is the energy needed to separate two atoms.
Tabulated bond enthalpies are average values calculated from the dissociation of many different compounds.
Thus tabulated bond enthalpies are approximate values.*However, they can be useful for approximating enthalpies of reaction because
most of the chemical energy of a compound is held in its bonds.*Work Reexamined
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Isochoric Work
pV work involves a volume change. Since a constant volume process has no volume change, w = 0 if there is no other work (no non-pV work).
No other assumptions have been made about the system.
Isobaric Work
Since the pressure is constant, it has no dependence on the volume. Thus the pressure can pulled out of the integral. Subsequently, the integral of dV is V2 – V1 = V
The only other assumption made is that the system does not have any non-pV work.
Isothermal Work
In general we need to know the relationship between pressure and volume to perform the calculation, i.e, we need an equation of state. Let us do the calculation for an ideal gas under reversible conditions.
Note restrictions on the applicability of the calculation.1. no other non-pV work2. ideal gas3. reversible conditions
Adiabatic Work
No assumptions made!
Refrigeration and the Joule-Thomson coefficient
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Joule coefficient -
- internal pressure
q = 0, w = 0 U = 0 isoenergetic process
Joule-Thomson coefficient -
- isoenthalpic, adiabatic- = 0 for an ideal gas
Classic Experimental Apparatus- measure JT directly.
Modern Experimental Apparatus
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- measure JT via
- use isothermal conditions rather adiabatic conditions.
isothermal conditions: T1 = T2
Isoenthalps on T- p plot.- inversion temperature
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- > 0 for substance to be used as a refrigerant- temperature must decrease as pressure decreases.
Real Gases Reexamined
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Calculations on van der Waals gas- pV work
- Difference in heat capacities
Internal Energy Reexamined
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Why is U = q v under isochoric conditions?
Assuming no non-pV work.
Isobaric Internal Energy
Note: no assumptions about the equation of state.
Isochoric Internal Energy
Note: assumption of no non-pV work
Isothermal Internal Energy
Enthalpy Reexamined
Why is H = q p under isobaric conditions?
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Assuming no non-pV work and reversible conditions
Isobaric Enthalpy
Assuming no non-pV work and reversible conditions
Isochoric Enthalpy
For ideal gas under reversible conditions
Why not ?
- temperature has a dependence on the pressure.
Isothermal Enthalpy
Important: All of the above enthalpies assume that the system has no non-pV work and reversible conditions (so that P = Pex)
Summary
Isothermal T = 0
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Isobaric p = 0Isochoric V = 0Adiabatic q = 0
Definition of work:
Definitions for heat: qp = H qV = U
Sign conventions for heat and work.
-w – work done by system (expansion for pV work)+w – work done on the system (compression for pV work)
-q – heat transferred away from body (heat lost)+q – heat transferred into body (heat gained)
Reversibilityp = pex
Extent of Reaction
Definition of Heat Capacities
First Law:
Partial Derivatives to be acquainted with: , , Cp, Cv, T, J, JT
and internal pressure (equals zero for ideal gas)
Natural variables of U and H and total differentials
Internal energy can be expressed as a function of V and T U(V,T)
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Enthalpy can be expressed as a function of p and T H(p,T)- both of these functional dependences are not unique- will consider other natural variables in the next chapter.
Total differential can be expressed as
Hess’ law
Temperature Dependence of Enthalpy and Internal Energy